EP0060212B1 - Tray drying chamber - Google Patents
Tray drying chamber Download PDFInfo
- Publication number
- EP0060212B1 EP0060212B1 EP82730022A EP82730022A EP0060212B1 EP 0060212 B1 EP0060212 B1 EP 0060212B1 EP 82730022 A EP82730022 A EP 82730022A EP 82730022 A EP82730022 A EP 82730022A EP 0060212 B1 EP0060212 B1 EP 0060212B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tray
- drying chamber
- truck
- drying
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000001035 drying Methods 0.000 title claims description 59
- 239000007789 gas Substances 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 6
- 210000002445 nipple Anatomy 0.000 claims description 5
- 239000011261 inert gas Substances 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 238000009827 uniform distribution Methods 0.000 claims 1
- 239000000463 material Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
- F26B9/066—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers the products to be dried being disposed on one or more containers, which may have at least partly gas-previous walls, e.g. trays or shelves in a stack
Definitions
- This invention relates to a drying installation for thermal drying.
- a drying apparatus consisting of a drying chamber and a tray-truck positioned within the drying chamber has been described in FR-A--2,311,637.
- This apparatus is constructed for drying wood, wherein a ventilator is placed at the rear of the drying chamber in a way that the impeller projects into the opening of the rear side of the tray-truck which has a rectangular form, whereas the drying chamber has a cylindrical shape.
- a drying device for drying a web of cloth on a heated rotating drum has been described in FR-A-2,355,258.
- tray-type drying chambers with recirculated air are frequently employed.
- the moist material is typically spread on specially shaped plates, so-called trays, which in turn are stacked on racks.
- the racks in most cases include casters or other rolling means on the bottom, so that the term tray-trucks is commonly employed to describe this structure.
- the tray-truck filled with trays is normally exposed within the tray drying chamber to an air stream which has been heated in a separate heating register.
- the warm air stream is conducted in a manner such that the largest portion thereof, i.e. in the range of 70-80 %, is recirculated, and the remaining, i.e.
- the residual moisture content of the moist material to be dried also includes organic chemical solvents, instead of just water, then these solvents can be condensed in a separate condenser within the drying chamber, while the drying of the material is being conducted, in order to protect the environment.
- organic chemical solvents instead of just water
- these solvents can be condensed in a separate condenser within the drying chamber, while the drying of the material is being conducted, in order to protect the environment.
- loose particles of the material to be dried are usually, in part, entrained in dust form, preferably adhering to the moist condenser in the chamber.
- the drying chamber of the invention is comprised primarily of two functionally unitary parts. More specifically, these two parts are the drying chamber proper, illustrated in Figure 1, and the tray-truck, illustrated in Figure 2.
- the structure of the two parts are so functionally related that only when the tray-truck is positioned within the drying chamber proper, are the gas-conducting channels defined to establish the specific gaseous flow paths which are necessary to conduct the drying process properly and/or for the conducting the gas therethrough.
- the tray-truck and the drying chamber fit flush together.
- the fitting is within the tolerance of manufacturing, practically, 1 to 5 mm.
- the clearance between the tray truck and the walls of the drying chamber effects a stray gaseous stream of 5 to 20 %. This deviation must be compensated by an augmented amount of gas passing over the moist material.
- Optimal drying is achieved at a gas flow of 0.1 to 2 m/s.
- the drying chamber is of a construction such that all walls, including the roof 3 and the floor 4, can be independently temperature-controlled.
- the drying chamber is constructed in a way such that the rear wall 5, and the two sidewalls 6 and 7 can be temperature-controlled.
- the walls are made of double-jacketed sheet metal, preferably stainless steel, through which the coolant, such as cooling water or cooling brine and/or the heating medium, such as hot water or steam, is conducted.
- suitable materials include steel sheet, provided with an organic protective coating, such as varnish or "Teflon".
- the tray-truck with casters or wheels is made up of closed side parts 13, a floor 11, and a roof 10.
- a rear wall 8 serves for regulating the direction of flow of the gaseous stream, and can be shaped as either one of a slotted wall, a finned wall, or a perforated wall.
- the rear wall 8 functions effectively as a control plate and will be referred to hereinafter as such.
- Baffle 9 is located spaced a predetermined distance behind the control plate 8, and the baffle is tightly sealed with respect to the roof but open toward the floor 11.
- the tray plates 12 are supported in the tray-truck on guiding angle members attached to the sidewalls 13 of the tray-truck. This means for supporting the tray plates is not shown and is conventional in nature. Other support structures can also be used as will become obvious to the skilled artisan.
- an inert gas such as nitrogen, is first of all introduced through a sealable feeding nipple to create an inert atmosphere in the chamber 14 for obvious safety reasons.
- a fan 15 with a vertically arranged shaft is located with the drive wheel 16 thereof integrally secured to the roof 3 of the drying chamber.
- the fan 15 serves to drive the gaseous stream along the heated rear wall 5 of the drying chamber, and the gaseous stream is heated as a result of this contact.
- the heated gas then rises through the space defined between the baffle 9 and the control plate 8 and is conducted through the control plate 8 and between the stacks of the tray plates 12, during which procedure the gas becomes saturated with the organic solvent which has been vaporized as a result of contact with the heated gas.
- the gas then passes the zone between the door of the drying chamber and the front end of the tray-truck, as shown in Figure 3, and the gas flows over the roof 10 of the tray-truck and below the roof 3 of the chamber past the drive wheel 16. After passing downstream of the drive wheel 16, and still upstream of the rear wall 5, a portion of the gaseous stream is branched off and conducted to the cooled sidewalls 6 and 7.
- the partial gas stream is diverted from the main stream behind the fan 15 by means of flaps, one for each wall 6 and 7, at an amount of 5 to 10 %.
- the gas is cooled on the side walls to a temperature below the dew point of the gas stream, and the solvent is condensed thereon.
- the temperature control of the side walls is effected in accordance with the particular solvent present, and as can be seen, is conventional in nature.
- the condensate is then collected on the lower portions of the sidewalls 6 and 7, which are shaped so as to collect the liquid, and from there it is drained off by means of discharge outlets 29 and 31.
- the drying chamber of this invention can, of course, also be utilized for the drying of water- moist products with no organic solvents, in which case the drying step can be carried out with fresh air rather than an inert gas, and in this case the air is exhausted, after being circulated, through the sealable exhaust air nipple 17 by way of the roof.
- the chamber be maintained totally sealed with respect to escaping gas because fresh air is plentiful and inexpensive to supply, whereas with an inert atmosphere, conservation of the inert gas containing gaseous organic solvents is desired.
- the drying chamber When working with an inert atmosphere, the drying chamber is under pressure in the range of 10- 3 to 2 x 10- 2 at.
- top wall 3 and rear wall 5, and optionally the front door (not shown) and the floor are associated with conduits extending to the double wall section thereof through which a hot fluid, such as steam, is supplied thereto by means of inlet 21, and removed by means of outlet 23.
- a hot fluid such as steam
- the sidewalls 6 and 7 are cooled by a supply of cooling fluid such as cold water by means of inlet 25 and outlet 27.
- the drying chamber of this invention has the advantage that, as compared to the prior art devices of comparable drying capacity, it is relatively small in size because auxiliary accessories, such as heating and/or cooling registers with the associated gas-conducting conduits are not required. Furthermore, all areas inside the chamber are readily accessible by simply moving the tray-truck out of the chamber, and thus, can be easily cleaned.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813109458 DE3109458A1 (de) | 1981-03-09 | 1981-03-09 | Hordentrockenschrank |
DE3109458 | 1981-03-09 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0060212A1 EP0060212A1 (en) | 1982-09-15 |
EP0060212B1 true EP0060212B1 (en) | 1986-02-19 |
Family
ID=6127031
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP82730022A Expired EP0060212B1 (en) | 1981-03-09 | 1982-03-05 | Tray drying chamber |
Country Status (6)
Country | Link |
---|---|
US (1) | US4459763A (enrdf_load_stackoverflow) |
EP (1) | EP0060212B1 (enrdf_load_stackoverflow) |
JP (1) | JPS57202478A (enrdf_load_stackoverflow) |
BR (1) | BR8201232A (enrdf_load_stackoverflow) |
DE (2) | DE3109458A1 (enrdf_load_stackoverflow) |
DK (1) | DK157258C (enrdf_load_stackoverflow) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0266516A3 (de) * | 1986-11-05 | 1989-03-29 | Hermann Waldner GmbH & Co. | Trockner, insbesondere für die chemische Industrie |
EP0775882A1 (de) | 1995-11-21 | 1997-05-28 | Hermann Waldner GmbH & Co. | Trockner, insbesondere für die chemische oder pharmazeutische Industrie |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8318604D0 (en) * | 1983-07-08 | 1983-08-10 | Newsome Air Conditioning | Cooling apparatus |
US5173316A (en) * | 1989-03-03 | 1992-12-22 | Heycott William B | Method for preparing fish bait |
US5003143A (en) * | 1990-04-09 | 1991-03-26 | Progressive Recovery, Inc. | Microwave sludge drying apparatus and method |
US5191722A (en) * | 1992-06-22 | 1993-03-09 | Her Majesty The Queen In Right Of Canada, As Represented By The Province Of Ontario | Method and arrangement for drying of fire hoses |
AU1153597A (en) * | 1996-10-23 | 1998-05-15 | Marvin Feldman Karpa | Air circulating cigar humidor |
US5878508A (en) * | 1997-01-10 | 1999-03-09 | American Harvest, Inc. | Food dehydrator |
CN2749501Y (zh) * | 2004-11-18 | 2006-01-04 | 黄明光 | 抽拉式多功能循环消毒柜 |
CN106705595A (zh) * | 2017-03-14 | 2017-05-24 | 苏州聚晶科技有限公司 | 一种温控烘干机 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2899189A (en) * | 1959-08-11 | Apparatus for processing compressed fuel | ||
US1282822A (en) * | 1915-11-10 | 1918-10-29 | Gordon Don Harris | Tunnel-drier. |
CH127092A (de) * | 1927-08-05 | 1928-08-01 | Alois Schilter | Zu Wärm- und Kühlzwecken verwendbarer Schrank. |
US2921382A (en) * | 1957-10-23 | 1960-01-19 | Louis L Blum | Shrimp preparing machine |
IT1032926B (it) * | 1975-05-19 | 1979-06-20 | Pagnozzi Ernesto Guglielmo | Procedimento a vuoto per essiccare legname massiccio particolarmente per essiccare legname delicato e o facilmente collassabile |
DE7618897U1 (de) * | 1976-06-15 | 1976-12-09 | Boewe Boehler & Weber Kg Maschinenfabrik, 8900 Augsburg | Trommeltrockner mit einer in einem gehaeuse um eine achse rotierbare trommel |
JPS5436367Y2 (enrdf_load_stackoverflow) * | 1976-10-23 | 1979-11-02 | ||
JPS5624389Y2 (enrdf_load_stackoverflow) * | 1978-02-23 | 1981-06-08 |
-
1981
- 1981-03-09 DE DE19813109458 patent/DE3109458A1/de not_active Withdrawn
-
1982
- 1982-02-25 DK DK083182A patent/DK157258C/da not_active IP Right Cessation
- 1982-03-05 DE DE8282730022T patent/DE3269117D1/de not_active Expired
- 1982-03-05 EP EP82730022A patent/EP0060212B1/en not_active Expired
- 1982-03-08 US US06/355,294 patent/US4459763A/en not_active Expired - Lifetime
- 1982-03-08 BR BR8201232A patent/BR8201232A/pt not_active IP Right Cessation
- 1982-03-08 JP JP57035270A patent/JPS57202478A/ja active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0266516A3 (de) * | 1986-11-05 | 1989-03-29 | Hermann Waldner GmbH & Co. | Trockner, insbesondere für die chemische Industrie |
US4837945A (en) * | 1986-11-05 | 1989-06-13 | Hermann Waldner Gmbh & Co. | Dryer, particularly for the chemical industry |
EP0775882A1 (de) | 1995-11-21 | 1997-05-28 | Hermann Waldner GmbH & Co. | Trockner, insbesondere für die chemische oder pharmazeutische Industrie |
Also Published As
Publication number | Publication date |
---|---|
JPS57202478A (en) | 1982-12-11 |
EP0060212A1 (en) | 1982-09-15 |
JPH0221516B2 (enrdf_load_stackoverflow) | 1990-05-15 |
DK157258C (da) | 1990-04-30 |
DE3109458A1 (de) | 1982-09-23 |
DE3269117D1 (en) | 1986-03-27 |
DK157258B (da) | 1989-11-27 |
DK83182A (da) | 1982-09-10 |
BR8201232A (pt) | 1983-01-18 |
US4459763A (en) | 1984-07-17 |
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